US3770527A - Nitranium perchlorate reaction rate alteration - Google Patents

Nitranium perchlorate reaction rate alteration Download PDF

Info

Publication number
US3770527A
US3770527A US00878591A US3770527DA US3770527A US 3770527 A US3770527 A US 3770527A US 00878591 A US00878591 A US 00878591A US 3770527D A US3770527D A US 3770527DA US 3770527 A US3770527 A US 3770527A
Authority
US
United States
Prior art keywords
cation
anion
perchlorate
nitronium perchlorate
rate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US00878591A
Inventor
J Maycock
L Witten
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Martin Marietta Corp
Original Assignee
Martin Marietta Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Martin Marietta Corp filed Critical Martin Marietta Corp
Application granted granted Critical
Publication of US3770527A publication Critical patent/US3770527A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B43/00Compositions characterised by explosive or thermic constituents not provided for in groups C06B25/00 - C06B41/00

Definitions

  • This invention relates to methods of altering the chemical reaction rates of materials, and to new materials obtained by such methods. More particularly, it relates to methods for altering the structure of existing high energy materials so that their chemical reaction rates may be either increased or decreased as desired.
  • High energy materials for the purposes of this discussion are those that under appropriate conditions undergo substantial exoenergetic, usually exothermic, reactions. These include explosives, fuels, and propellant oxidizers.
  • Solid materials containing point defects include both materials in which the bonding is purely ionic and materials, such as lead. azide, in which the bond is partly covalent and partly ionic.
  • These materials are comprised of anions and cations held in a regular lattice structure by ionic bonds or by a combination of ionic and covalent bonding.
  • the materials that are amenable to the process of this invention may not all be normally considered as crystals when the word is used in its loose sense to describe a material having crystalline structure on a macro scale. Rather, the crystalline structure referred to is the basic structure of the material, and may exist only on a micro scale, as, for instance, when the material is powdered.
  • ion vacancies positions in the crystalline structure that would normally be occupied by an anion or cation but which are in fact vacant.
  • Such ion vacancies bear an effective charge of a polarity opposite to that of the ion that would occupy that site if the lattice structure were regular, or perfect.
  • a cation vacancy would accordingly have an effective negative charge and an anion vacancy, an effective positive charge.
  • the chemical reactions of such materials may be complex in nature and the overall reaction may include a series of individual reactions.
  • all chemical reactions of solids containing point defects are characterized by the loss of electrons by the anions, these electrons being subsequently captured by the vacant lattice sites that are created by anion vacancies and that form effective positive charges.
  • the greater the number of anion vacancies in the material the faster the rate of electron capture and the faster the rate of chemical reaction.
  • the chemical reaction rate may be increased by increasing the number of anion vacancies in the solid, or by decreasing the number of cation vacancies.
  • An increase in the number of cation vacancies, or a decrease in the number of anion vacancies, will tend to slow down the chemical reaction and decrease the reaction rate.
  • the number of lattice site vacancies may be adjusted by replacing some of the ions with ions having the same polarity but a different valence.
  • a solid composed of univalent anions and univalent cations Suppose it is desired to increase the chemical reaction rate of the solid. As described above, this may be accomplished by increasing the number of anion lattice site vacancies. To do this, we replace some of the univalent anions in the lattice structure with anions having a greater valence, say divalent anions. Since the solid must remain electrically neutral, the additional charge incorporated by the divalent anions will be balanced by the loss of univalent anions;
  • the univalent cations are replaced with divalent cations that are less colored than the host material, that is, that absorb light at wavelengths shorter than the wavelengths at which the host material absorbs light, the number of cation vacancies increases and the chemical reaction rate is decreased.
  • univalent ions could also be replaced by ions having a valence greater than two. Also, in a solid composed of ions having a valence greater than one, some of the ions could be replaced by ions having a lower valence. This latter replacement would generally have an opposite effect on the reaction rate than replacement with ions having a greater valence.
  • the original solid and a material containing the replacement ions may both be dissolved in a suitable solvent. Crystals obtained from the solution, as by cooling it, will then have the desired characteristics.
  • the following examples describe in detail the operation of the process.
  • the crystals that had precipitated were filtered off and dried for about 24 hours under a vacuum of about mm of H
  • The-chemical reaction rate of the crystals obtained bythis process was compared with the reaction rate of pure nitronium perchlorate crystals by comparing the relative periods of time required for the pressure of oxygen (O evolved from thermal decomposition to cover a specified pressure range when the materials thermally decomposed at a constant temperature and in a closed volume container.
  • O evolved from thermal decomposition to cover a specified pressure range when the materials thermally decomposed at a constant temperature and in a closed volume container.
  • the rate of thermal decomposition of the resulting crystals was compared to the thermal decomposition rate of pure nitronium perchlorate crystals in the same manner as in Example 1.
  • 4.5 minutes were required for the oxygen (0 pressure resulting from the pure nitronium perchlorate decomposition to increase from 15 p. to 40 ;1.
  • 6.7 minutes were required to cover the same pressure range under the same conditions by the oxygen (0 evolved from decomposition of the crystals obtained from the process of this example.
  • 5.2 minutes were required by the oxygen (0 evolved from pure nitronium perchlorate and H2 minutes for the oxygen (0 evolved from the crystals of the process of this example.
  • Example 2 At the same constant temperature and in the same closed volume as in Example 2 (C. and 2.2 liters, respectively), the oxygen (0 evolved from the pure nitronium perchlorate crystals required (as in Example 2) 4.5 minutes to increase in pressure from 15 p. to 40 p. and 5.2 minutes to increase from 100 p. to 300 u.
  • the rate of decomposition of the resulting crystals was compared to the rate of decomposition of pure ammonium perchlorate (NH ClO crystals as in the previous examples, by comparing the length of time required for oxygen (0 evolved during decomposition to cover a prescribed range of pressures while maintained at a constant temperature.
  • the decomposition rate is of course a function of temperatures, and these comparisons were carried out at a number of temperatures. The results of the comparisons for two temperatures are set forth in the following table:
  • the substituted ion should be thermally stable at the temperature of thermal decomposition of the original material.
  • the general procedure used in the preceding examples is a convenient one.
  • the replacement ion forms part of a salt that is dissolved in a common solvent along with the original material
  • the resulting crystalline material might also have Y ions substituted for B ions, which would tend to vitiate or cancel out the decrease in reaction rate intended to be accomplished by substituting the X divalent cation for A univalent cation.
  • a process for accelerating the rate of thermal decomposition of nitronium perchlorate comprising cocrystallizing with it about 0.001 to about mole percent of a foreign anion that is thermally stable at the temperature of decomposition of said nitronium perchlorate and that has a valence state greater than one, and a corresponding amount of a cation having a valence less than the valence of said. anion.
  • a process for decelerating the rate of thermal decomposition of nitronium perchlorate comprising cocrystallizing with it about 0.001 to about 20 mole percent of a foreign cation that a. has a valence state greater than one, b. is thermally stable at the temperature of decomposition of said nitronium perchlorate, and c. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbs light, and the corresponding amount of an anion that a. has a valence state less than the valence state of said cation, and b.
  • the novel composition of matter of claim 6 wherein said anion is 8.
  • the novel composition of matter comprising a nitronium perchlorate lattice having in ionic distribution therein about 0.001 to about 20 mole percent of a foreign cation that a. has a valence state greater than one, b. is thermally stable at the temperature of decomposition of said nitronium perchlorate, and c. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbs light, and the corresponding amount of an anion that a. has a valence state less than the valence state of said cation, and b. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbe light.
  • said cation is Ca.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

The rate of thermal decomposition of certain high energy solid state materials, such as nitronium oxidizers, may be either increased or decreased by doping to replace ions in the structure with ions having a different valence. Decompsoition rate is increased if univalent anions are replaced with multivalent anions, and rate is conversely decreased if univalent cations are replaced with multivalent cations that are less colored than the host material.

Description

United States Patent Maycock et al. Nov. 6, 1973 [54] NITRANIUM PERCHLORATE REACTION 3,167,386 1/1965 McElroy et al. 23/85 X RATE ALTERATION 3,186,790 6/1965 Brovvn et a1. 23/85 X 2,190,703 2/1940 Davis 149/76 X [75] Invent rs: John Norman May m r 3,172,793 3/1965 Markowitz 1 149/19 Md.; Louis Witten, Cincinnati, Ohio 3,418,183 12/1968 Rice 149/6 [73] Assignee: Martin Marietta Corporation, New OTHER PUBLICATIONS York Verneker eta1., .1. Inorganic NucL. Chem., Vol. 29, pp. [22] Filed: Nov. 20, 1969 2729-2730 (1967).
[21] Appl' 878591 Primary ExaminerCar1 D. Quarforth Related US. Application Data Assistant Examiner-E. A. Miller [63] Continuation-in-part of Ser. No. 589,185, Oct. 19, n ym B- EiSel an Gay Chin 1966. 52 U S Cl 149/74 149/75 149/76 [57] ABSTRACT 1 The rate of thermal decom osition of certain high en- 423/386 P [51] Int CL C06b 11/00 ergy solid state materials, such as nitronium oxidizers, [53] Field 49/76 74 may be either increased or decreased by doping to replace ions in the structure with ions having a different valence. Decompsoition rate is increased if univalent [56] References Cited anions are replaced with multivalent anions, and rate is conversely decreased if univalent cations are replaced UNITED STATES PATENTS with multivalent cations that are less colored than the 1,284,328 15/1913 lbs/1e gueur host i L 3,l47,l 196 c rone 3,269,879 8/1966 Stammlcr et a1 149/2 10 Claims, N0 Drawings NlTlRANllUM PERCHLORATE REACTllON RATE ALTERATION This application is a continuation-in-part of our copending application, Ser. No. 589,185, filed Oct. 19, 1966.
This invention relates to methods of altering the chemical reaction rates of materials, and to new materials obtained by such methods. More particularly, it relates to methods for altering the structure of existing high energy materials so that their chemical reaction rates may be either increased or decreased as desired. High energy materials for the purposes of this discussion are those that under appropriate conditions undergo substantial exoenergetic, usually exothermic, reactions. These include explosives, fuels, and propellant oxidizers.
The desirability of modifying the chemical reaction rates of such materials has long been recognized. Various applications of military and commercial explosives require different explosive characteristics and for years the chemical reaction rates of explosives have been adjusted to provide these characteristics. Reaction rate alterations have also been performed to render a high energy material suitable for entirely different applications. For instance, the chemical reaction rates of materials generally used as explosives have been slowed to create materials suitable for rocket propellants. The chemical reaction rates of both explosives and oxidizers have been both increased and decreased.
Prior art modifications of the chemical reaction rates of high energy materials generally suffer from one or more limitations. Such modification has been usually accomplished by mechanical mixing of an additional ingredient or ingredients with the high energy materials. Such mixing has disadvantages. The additional in gredient, while providing the desired chemical reaction rate, may affect other characteristics of the material unfavorably. Also, high energy materials are often combined with binders and the like to form charges, or for other purposes, and the additives for altering reaction rates often react disadvantageously with these other materials. A trade-off must therefore be made between the advantages of reaction rate change and the concomitant degradation of other desirable characteristics. Further, it is difficult in such mechanical mixing to achieve the ultimate in uniform dispersion, and uneven reactions often result from the consequent inhomogeneity.
Prior art methods of modifying chemical reaction rates are generally quite specific: usually a particular additive will work with only one or a small, closely related group, of high energy materials. No overall approach has been developed that is usable for all or a large group of high energy materials, and that will permit the reaction rate to be increased or decreased,
whichever is desired. I
It is an object of this invention to provide a method of altering the chemical reaction rate of a large group of solid materials, including many high energy materials.
it is a further object of this invention to provide such a method that will permit the chemical reaction rate to be either increased or decreased, as desired, and that will result in smooth and even reactions.
it is still another object of this invention to provide certain high energy materials that have more desirable chemical reaction rates as a result of modification by this method.
We have discovered a method for altering the chemical reaction rate of a solid material containing point defects which is rich in at least one gaseous element and capable of thermally decomposing into completely gaseous products. Solid materials containing point defects include both materials in which the bonding is purely ionic and materials, such as lead. azide, in which the bond is partly covalent and partly ionic.
These materials are comprised of anions and cations held in a regular lattice structure by ionic bonds or by a combination of ionic and covalent bonding. The materials that are amenable to the process of this invention may not all be normally considered as crystals when the word is used in its loose sense to describe a material having crystalline structure on a macro scale. Rather, the crystalline structure referred to is the basic structure of the material, and may exist only on a micro scale, as, for instance, when the material is powdered.
The point defects contained in these solids are ion vacancies; that is, positions in the crystalline structure that would normally be occupied by an anion or cation but which are in fact vacant. Such ion vacancies bear an effective charge of a polarity opposite to that of the ion that would occupy that site if the lattice structure were regular, or perfect. A cation vacancy would accordingly have an effective negative charge and an anion vacancy, an effective positive charge.
The chemical reactions of such materials may be complex in nature and the overall reaction may include a series of individual reactions. However, all chemical reactions of solids containing point defects are characterized by the loss of electrons by the anions, these electrons being subsequently captured by the vacant lattice sites that are created by anion vacancies and that form effective positive charges. The greater the number of anion vacancies in the material, the faster the rate of electron capture and the faster the rate of chemical reaction.
The chemical reaction rate may be increased by increasing the number of anion vacancies in the solid, or by decreasing the number of cation vacancies. An increase in the number of cation vacancies, or a decrease in the number of anion vacancies, will tend to slow down the chemical reaction and decrease the reaction rate.
The number of lattice site vacancies (point defects) may be adjusted by replacing some of the ions with ions having the same polarity but a different valence. Consider a solid composed of univalent anions and univalent cations. Suppose it is desired to increase the chemical reaction rate of the solid. As described above, this may be accomplished by increasing the number of anion lattice site vacancies. To do this, we replace some of the univalent anions in the lattice structure with anions having a greater valence, say divalent anions. Since the solid must remain electrically neutral, the additional charge incorporated by the divalent anions will be balanced by the loss of univalent anions;
that is, by an increase in the number of anion vacancies in the lattice.
If some of the univalent cations are replaced with divalent cations that are less colored than the host material, that is, that absorb light at wavelengths shorter than the wavelengths at which the host material absorbs light, the number of cation vacancies increases and the chemical reaction rate is decreased.
Obviously, we are not limited to replacing univalent ions with divalent ions in order to alter the number of lattice site vacancies, although this type of substitution would be probably the most used. Univalent ions could also be replaced by ions having a valence greater than two. Also, in a solid composed of ions having a valence greater than one, some of the ions could be replaced by ions having a lower valence. This latter replacement would generally have an opposite effect on the reaction rate than replacement with ions having a greater valence. lf divalent anions were replaced with univalent anions that are less colored than the host material, that is, that absorb light at wavelengths less than the wavelength at which the host material absorbs light, the number of anion vacancies would decrease, and the reaction rate would also decrease. And if divalent cations were replaced with univalent cations, the number of cation vacancies would decrease, and the reaction rate would increase.
in order to effect the ion replacement described, the original solid and a material containing the replacement ions may both be dissolved in a suitable solvent. Crystals obtained from the solution, as by cooling it, will then have the desired characteristics. The following examples describe in detail the operation of the process.
EXAMPLE 1 The chemical reaction rate of nitronium perchlorate (NO ClO was decreased by the substitution of divalent strontium cations (Sr for the univalent nitronium cations (NOJ) on approximately a 10' mole ratio. Ten grams of nitronium perchlorate (NO ClO and 100 milligrams of strontium chloride (SrCl were placed in 10 milliliters of undiluted nitric acid (HN at room temperature. The solution temperature was raised to 70C., at which point all of the solids were dissolved in the solution. The solution was then permitted to cool to room temperature. The crystals that had precipitated were filtered off and dried for about 24 hours under a vacuum of about mm of H The-chemical reaction rate of the crystals obtained bythis process was compared with the reaction rate of pure nitronium perchlorate crystals by comparing the relative periods of time required for the pressure of oxygen (O evolved from thermal decomposition to cover a specified pressure range when the materials thermally decomposed at a constant temperature and in a closed volume container. When the same weight of both materials was thermally decomposed in a closed volume of 1.3 liters at a constant temperature of 80C., it required 1.2 minutes for the oxygen pressure resulting from pure nitronium perchlorate crystal decomposition to go from 0.01 p. to 0.25 while it required 7.5 minutes for the oxygen pressure from thermal decomposition of the crystals produced by this process to cover the same range under the same conditions.
EXAMPLE 2 The chemical reaction rate of nitronium perchlorate (NO CIO was decreased by substituting divalent cations of calcium (Ca*") for the univalent cations of nitronium (NO on approximately a l0- mole ratio. The process was identical to that described in Example 1 except that 113 milligrams of calcium nitrate (Ca(- N09 was substituted for the strontium chloride of Example 1.
The rate of thermal decomposition of the resulting crystals was compared to the thermal decomposition rate of pure nitronium perchlorate crystals in the same manner as in Example 1. At a constant temperature of 120C. and in a closed volume of 2.2 liters, 4.5 minutes were required for the oxygen (0 pressure resulting from the pure nitronium perchlorate decomposition to increase from 15 p. to 40 ;1., whereas 6.7 minutes were required to cover the same pressure range under the same conditions by the oxygen (0 evolved from decomposition of the crystals obtained from the process of this example. For the pressure range of p. to 300 ,2, under the same conditions, 5.2 minutes were required by the oxygen (0 evolved from pure nitronium perchlorate and H2 minutes for the oxygen (0 evolved from the crystals of the process of this example.
EXAMPLE 3 The chemical reaction rate of nitronium perchlorate (NO CIO was increased by the substitution of divalent sulfate anions ($0 for the univalent perchlorate anions (ClOf) on approximately a 10 mole ratio. The process was identical to that of Examples 1 and 2 except that 91 milligrams of ammonium sulfate ((NH SO,,) was mixed with the 10 grams of nitronium perchlorate (NO ClO in the 10 milliliters of undiluted nitric acid (HNO The rate of thermal decomposition of the crystals obtained by the process of this example was compared with the decomposition rate of pure nitronium perchlorate crystals in a manner similar to that of Examples 1 and 2. At the same constant temperature and in the same closed volume as in Example 2 (C. and 2.2 liters, respectively), the oxygen (0 evolved from the pure nitronium perchlorate crystals required (as in Example 2) 4.5 minutes to increase in pressure from 15 p. to 40 p. and 5.2 minutes to increase from 100 p. to 300 u. The oxygen evolved from the decomposition of the crystals produced by the process of this example, however, required only 3.0 minutes to increase in pressure from 15 y. to 40 IL and only 3.5 minutes to increase from 100 p. to 300 u.
EXAMPLE 4 The chemical reaction rate of ammonium perchlorate (NH ClO was reduced by substituting divalent cations of calcium (Ca**) for the univalent cations of ammonium (NI-l on approximately a 10 mole ratio. Ten grams of ammonium perchlorate (NH ClO,) and 100 milligrams of calcium nitrate (Ca(NO were placed in 25 milliliters of distilled water at room temperature. the temperature of the solution was raised to 90C., at which point all of the solids were dissolved in the solution. The solution was then permitted to cool to room temperature. The crystals that had precipitated were filtered off and dried for about 24 hours under a vacuum of about 10 mm of H After vacuum drying, the crystals were heated in an oven maintained at between 1 l0l 30C. for about four hours to remove any remaining water.
The rate of decomposition of the resulting crystals was compared to the rate of decomposition of pure ammonium perchlorate (NH ClO crystals as in the previous examples, by comparing the length of time required for oxygen (0 evolved during decomposition to cover a prescribed range of pressures while maintained at a constant temperature. The decomposition rate is of course a function of temperatures, and these comparisons were carried out at a number of temperatures. The results of the comparisons for two temperatures are set forth in the following table:
Pressure Time for 0 Time for 0 from Pure from Crystals Temp. (C.) Range ([1.) NH ClO of this Process 225 50 to 100 min. 24 min. 250 50 to 100 2 min. 4 min.
Where the chemical reaction rate comprises thermal decomposition, the substituted ion should be thermally stable at the temperature of thermal decomposition of the original material.
While other methods of effecting the substitution of the desired ion into the lattice structure are of course possible and within the contemplation of our invention, the general procedure used in the preceding examples is a convenient one. When, in accordance with this procedure, the replacement ion forms part of a salt that is dissolved in a common solvent along with the original material, it is desirable to make sure that the other ion with which the replacement ion is combined to form the salt does not operate to destroy the effect created by the desired replacement. For instance, consider an original material comprised of univalent ions A B', with the reaction rate to be decreased by replacing the A ion with X. if the X ion is to be substituted by dissolving A03 and X Y salts in a common solvent, then the resulting crystalline material might also have Y ions substituted for B ions, which would tend to vitiate or cancel out the decrease in reaction rate intended to be accomplished by substituting the X divalent cation for A univalent cation. Therefore, in performing a cation substitution by this method, it would be well either to use a salt of the form X (Z) with a univalent anion coupled with the divalent cation, or, if a divalent anion Y- is to be used, make sure that it is not compatible with the AER crystalline structure and therefore will not be substituted in the lattice for B" anions.
As the above description and examples make clear, we have discovered a new and powerful method for varying at will the chemical reaction rates of those solid materials having point defects, and new and useful materials formed by this process. Various modifications that will be obvious to those skilled in the art are within the contemplated scope of our invention, which is limited only by the appended claims.
We claim:
it. A process for accelerating the rate of thermal decomposition of nitronium perchlorate comprising cocrystallizing with it about 0.001 to about mole percent of a foreign anion that is thermally stable at the temperature of decomposition of said nitronium perchlorate and that has a valence state greater than one, and a corresponding amount of a cation having a valence less than the valence of said. anion.
2. The process of claim 1 wherein said anion is $0,. 3. A process for decelerating the rate of thermal decomposition of nitronium perchlorate comprising cocrystallizing with it about 0.001 to about 20 mole percent of a foreign cation that a. has a valence state greater than one, b. is thermally stable at the temperature of decomposition of said nitronium perchlorate, and c. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbs light, and the corresponding amount of an anion that a. has a valence state less than the valence state of said cation, and b. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbs light. 4. The process of claim 3 wherein said cation is Ca. 5. The process of claim 3 wherein said cation is Sr. 6. The novel composition of matter comprising a nitronium perchlorate lattice having; in ionic distribution therein about 0.001 to about 20 mole percent of a foreign anion that is thermally stable at the temperature of decomposition of said nitronium perchlorate and that has a valence state greater than one, and a corresponding amount of a cation having a valence less than the valence of said anion.
7. The novel composition of matter of claim 6 wherein said anion is 8. The novel composition of matter comprising a nitronium perchlorate lattice having in ionic distribution therein about 0.001 to about 20 mole percent of a foreign cation that a. has a valence state greater than one, b. is thermally stable at the temperature of decomposition of said nitronium perchlorate, and c. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbs light, and the corresponding amount of an anion that a. has a valence state less than the valence state of said cation, and b. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbe light. 9. The novel composition of matter of claim 8 wherein said cation is Ca.
10. The novel composition of matter of claim 8 wherein said cation is Sr.

Claims (9)

  1. 2. The process of claim 1 wherein said anion is SO4.
  2. 3. A process for decelerating the rate of thermal decomposition of nitronium perchlorate comprising cocrystallizing with it about 0.001 to about 20 mole percent of a foreign cation that a. has a valence state greater than one, b. is thermally stable at the temperature of decomposition of said nitronium perchlorate, and c. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbs light, and the corresponding amount of an anion that a. has a valence state less than the valence state of said cation, and b. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbs light.
  3. 4. The process of claim 3 wherein said cation is Ca .
  4. 5. The process of claim 3 wherein said cation is Sr .
  5. 6. The novel composition of matter comprising a nitronium perchlorate lattice having in ionic distribution therein about 0.001 to about 20 mole percent of a foreign anion that is thermally stable at the temperature of decomposition of said nitronium perchlorate and that has a valence state greater than one, and a corresponding amount of a cation having a valence less than the valence of said anion.
  6. 7. The novel composition of matter of claim 6 wherein said anion is SO4 .
  7. 8. The novel composition of matter comprising a nitronium perchlorate lattice having in ionic distribution therein about 0.001 to about 20 mole percent of a foreign cation that a. has a valence state greater than one, b. is thermally stable at the temperature of decomposition of said nitronium perchlorate, and c. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbs light, and the corresponding amount of an anion that a. has a valence state less than the valence state of said cation, and b. does not absorb light at a wavelength shorter than the wavelength at which nitronium perchlorate absorbe light.
  8. 9. The novel composition of matter of claim 8 wherein said cation is Ca .
  9. 10. The novel composition of matter of claim 8 wherein said cation is Sr .
US00878591A 1969-11-20 1969-11-20 Nitranium perchlorate reaction rate alteration Expired - Lifetime US3770527A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US87859169A 1969-11-20 1969-11-20

Publications (1)

Publication Number Publication Date
US3770527A true US3770527A (en) 1973-11-06

Family

ID=25372348

Family Applications (1)

Application Number Title Priority Date Filing Date
US00878591A Expired - Lifetime US3770527A (en) 1969-11-20 1969-11-20 Nitranium perchlorate reaction rate alteration

Country Status (1)

Country Link
US (1) US3770527A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20170271591A1 (en) * 2015-02-13 2017-09-21 Hewlett Packard Enterprise Development Lp Multilayered memristors

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1284380A (en) * 1917-12-29 1918-11-12 Ernest A Le Sueur Art of preparing ammonium perchlorate.
US2190703A (en) * 1938-03-08 1940-02-20 Du Pont Perchlorate explosive
US3147160A (en) * 1958-05-28 1964-09-01 Walter C Mccrone Desensitization of ammonium perchlorate
US3167386A (en) * 1961-02-10 1965-01-26 Callery Chemical Co Complex perchlorate compound and its production
US3172793A (en) * 1965-03-09 Temperature xc
US3186790A (en) * 1960-06-22 1965-06-01 Callery Chemical Co Production of nitronium perchlorate
US3269879A (en) * 1964-04-13 1966-08-30 Aerojet General Co Ammonium salt lattice with isomorphously substituted inorganic salts
US3418183A (en) * 1963-12-04 1968-12-24 Thiokol Chemical Corp Propellant comprising hydrazine nitroform stabilized with dicarboxylic acid anhydride

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3172793A (en) * 1965-03-09 Temperature xc
US1284380A (en) * 1917-12-29 1918-11-12 Ernest A Le Sueur Art of preparing ammonium perchlorate.
US2190703A (en) * 1938-03-08 1940-02-20 Du Pont Perchlorate explosive
US3147160A (en) * 1958-05-28 1964-09-01 Walter C Mccrone Desensitization of ammonium perchlorate
US3186790A (en) * 1960-06-22 1965-06-01 Callery Chemical Co Production of nitronium perchlorate
US3167386A (en) * 1961-02-10 1965-01-26 Callery Chemical Co Complex perchlorate compound and its production
US3418183A (en) * 1963-12-04 1968-12-24 Thiokol Chemical Corp Propellant comprising hydrazine nitroform stabilized with dicarboxylic acid anhydride
US3269879A (en) * 1964-04-13 1966-08-30 Aerojet General Co Ammonium salt lattice with isomorphously substituted inorganic salts

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Verneker et al., J. Inorganic Nucl. Chem., Vol. 29, pp. 2729 2730 (1967). *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20170271591A1 (en) * 2015-02-13 2017-09-21 Hewlett Packard Enterprise Development Lp Multilayered memristors
US10026896B2 (en) * 2015-02-13 2018-07-17 Hewlett Packard Enterprise Development Lp Multilayered memristors

Similar Documents

Publication Publication Date Title
US4875762A (en) Photochromic-electrochromic intercalation compound
US2590054A (en) Process of producing ammonium nitrate-containing composition
US4552736A (en) Potassium fluoride stabilized ammonium nitrate
US3819819A (en) Aluminum hydride in hexagonal or rhombohedral crystalline form
US3770527A (en) Nitranium perchlorate reaction rate alteration
US3149956A (en) Preparation of granular nitrogenous fertilizer
US4139404A (en) Active binder propellants incorporating burning rate catalysts
US3883644A (en) Aluminum hydride
US3173756A (en) Double nitrate salts and methods for their preparation
US3721590A (en) Ammonium perchlorate with cocrystallized oxalate anions
US3259531A (en) Propellant with ammonium perchloratepermanganate lattice oxidizer
Bagnall et al. 581. Some chloro-complexes of quinquevalent protactinium, niobium, and tantalum
US4108965A (en) (NF4)2 NiF6 High energy solid propellant oxidizer and method of producing the same
US3708357A (en) Oxidizers with improved thermal stability and method of making same
US3357788A (en) Process for producing finely divided calcium fluoride having controlled particle size
US2929680A (en) Preparation of lithium perchlorate
US1671792A (en) Method of impregnating absorptive material for use in explosives
US3159512A (en) Process for the production of primer compositions for percussion caps including rimfire cartridges
US2333637A (en) Explosive composition
US3567646A (en) Stable cesium compounds
US3066009A (en) Preparation of decaboranyl sodium
US3293091A (en) Complex salts of basic lead picrate
US3032405A (en) Process for making alkali metal metaborates and compositions containing the same
US4107275A (en) Method for producing NF4 BF4
US3167386A (en) Complex perchlorate compound and its production